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EP 2 818 581 B1 |
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EUROPEAN PATENT SPECIFICATION |
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Mention of the grant of the patent: |
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22.03.2017 Bulletin 2017/12 |
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Date of filing: 10.06.2014 |
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International Patent Classification (IPC):
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Method of manufacturing a synthetic gas by electrolysis of a particular electrolyte
Verfahren zur Herstellung eines synthetischen Gases durch Elektrolyse eines bestimmten
Elektrolyten
Procédé de fabrication d'un gaz de synthèse par électrolyse d'un électrolyte particulier
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Designated Contracting States: |
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AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL
NO PL PT RO RS SE SI SK SM TR |
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Priority: |
11.06.2013 IT VA20130034
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Date of publication of application: |
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31.12.2014 Bulletin 2015/01 |
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Proprietors: |
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- Ferrario, Diego
24043 Caravaggio (BG) (IT)
- Palermo, Giulio
23880 Casatenovo (LC) (IT)
- Aceti, Fabio
24059 Urgnano (BG) (IT)
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Inventor: |
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- Ferrario, Diego
24043 Caravagigio (IT)
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Representative: Forattini, Amelia |
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Internazionale Brevetti
Ingg. ZINI, MARANESI & C. S.r.l.
Piazza Castello 1 20121 Milano 20121 Milano (IT) |
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References cited: :
JP-A- 2000 144 464 US-A1- 2002 027 079
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JP-A- 2008 045 205 US-A1- 2005 269 210
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- ST JOHN M R ET AL: "Hydrogen Generation from Glucose Depolarized Water Electroysis",
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, ELECTROCHEMICAL SOCIETY, MANCHESTER, NEW HAMPSHIRE;
US, vol. 128, no. 5, 1 May 1981 (1981-05-01), pages 1174-1176, XP002423440, ISSN:
0013-4651, DOI: 10.1149/1.2127576
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Remarks: |
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The file contains technical information submitted after the application was filed
and not included in this specification |
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| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
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[0001] 0001. Nowadays there are gases that are produced by water electrolysis for a variety
of industrial and civil uses. In most cases this electro-chemical process produces
by cleavage an oxygen molecule and two hydrogenous molecules. These gases are usually
employed in various sectors both singularly (like oxygen for the hospitals) and mixed
with other gases (like hydrogenous mixed with lpg for the production of glass, or
with other gases for flame cutting).
[0002] 0002. So far no one could produce easy to manage combustible gases, non-explosive
and easily usable by a known method, like electrolysis.Today this problem is solved
thanks to a
Method of manufacturing a synthetic gas by electrolysis of a particular electrolyte, hereinafter called FOUND with which is obtained a combustible gas that can be used
directly and immediately in the current types of burners calibrated for the gas supply
network.
[0003] 0003. Additional features of this FOUND will be better highlighted through an analysis
of the description of an application shown in the indicative but not limitative, with
the help of the attached tables for: Method of manufacturing a synthetic gas by electrolysis
of a particular electrolyte
Table 1:
fig. A)-Is a schematic view of the electrolytic system
In which in a container (fig.A1) sealed by a lid (fig.A8) with a connection for gas
leakage (fig. A6); there is a liquid content (fig.A2) in which two electrodes are
immersed (fig.A4 and A5) connected to an electricity generator (fig.A3). The container
is connected to a heat exchanger with the function of cooling the electrolytic solution
(fig.A7).
Preparatory method
[0004] 0004. The fuel gas obtained from FOUND occurs, through the use of an electrolyzer
of the type used for the production of hydrogen / oxygen mixture also known with the
name "Brown gas" - with reference to the patent
US7.014,
740 B2-Inventor Sang-Nam Kim (KR) -. This type of electrolyzer is constituted by a container
sealing, inside which is normally installed a multiplicity of Cathodes alternating
Anodes arranged in an electrical series in which the cathode and the anode terminal
are connected respectively to the negative and positive poles of a DC rectifier.
[0005] 0005. In our specific case, the electrolyzer used in the experiment has the anodes
and cathodes of the size 15x15 cm with a thickness of 1 mm for a total of 14 plates;
positioned at a 3 mm. distance from each other. All built entirely in stainless steel
AISI 316.
[0006] 0006. The voltage applied to each pair of cathode / anode is between 2 and 3 Volts
with an intensity between 1.5 and 2.5 Ah.
In the electrolyzer is a mixture consisting of:
- 1000 ml of distilled water (H2O)
- from 10 to 50 g/l (grams per liter) of potassium hydroxide or sodium hydroxide; with
the function of electrolyte, necessary for the electrical conductivity
- from 20 to 100 g/l (grams per liter) of Ascorbic Acid (C6H8O6)
The operating temperature is between 60-70° C (Celsius)
[0007] 0007. By means of the electrolyte, a gas is generated mixture consisting of about
67% hydrogen (H), 26% of carbon dioxide (CO2), 2% Carbon Monoxide (CO), 2% oxygen.
The content of hydrocarbons such as methane, ethane / ethylene, propane / propylene,
other higher hydrocarbons and alcohols is limited to some 10 ppm / v.
[0008] 0008. The most interesting feature of this gas obtained through FOUND, is the characteristic
presence of Carbon Dioxide and Carbon Monoxide. The origin of these two elements is
attributed to the introduction in the electrolyte of Ascorbic Acid (C
6H
8O
6). In this case the process may be summarized as follows:
(anode) C
6H
8O
6+6H
2O → 3CO
2+ 20H
+ + 20 e-
(cathode) 20 H
+ + 20 e- → 10 H
2
[0009] 0009. During the process the starting electrolyte initially captures carbon dioxide
with intermediate formation of carbonate and potassium bicarbonate final: only after
the completion of these reactions will reach the free development of carbon dioxide
gas. Since there are no separators between cathodes and anodes, the cathode and anode
gases are mixed, giving origin to a gas composed by 70% hydrogen (H) and 30% of carbon
dioxide (CO2); whose chemical compound is the following:
H2(g) + O2(g) + CO(g) + CO2(g) + CH4(g)
+ CH2(g)-
+ C3H8(g)
+ C4H10(g)
+ C5H12(g)
+ CH3(CH2)4CH3(g)
+ CH3OH(g)
+ C2H6O(g)
+ CH3CH(OH)CH3(g)
+ C6H6(g)
+ C7H8(g)
+ C8H10(g)
+ C3H6O(g)
The gas produced from this process is colorless, odorless, it generates a transparent
combustion flame. The gas obtained has a high calorific value, it can be used both
as fuel for flames flowing or for internal combustion engines.
[0010] 0010. In laboratory experiments, it has been noticed in some cases, by chemical analysis
carried out on the gas generated by FOUND, the presence of traces of nitrogen N
2(g), probably due to an inadvertent contact of the gas generated with the air. Furthermore,
it has been noticed that if the temperature, during electrolysis, falls below the
degrees, some molecules are liquid instead of being in the gaseous state, anyway maintaining
an irrelevant percentage in the final chemical compound.
[0011] 0011. In the case of industrial production, the amount of the individual elements
of the basic solution may vary, as well as in place of potassium carbonate other types
of chemically similar salts can be used. The quantities of the individual components
may slightly vary.
[0012] 0012. The graphic description represented should be simply regarded as an example.
[0013] 0013. The types of equipment for the electrolysis may vary depending on the technical
and manufacturing needs, without prejudice to the inventive concept and the recipe
of the liquid solution to be used.
1. Method of production of a synthetic gas by electrolysis of a particular electrolyte
composed of a solution of demineralized water (H2O), potassium hydroxide (KOH) or
sodium hydroxide (NaOH), and ascorbic acid (C6H806), said solution composed of, for
each 1000 ml of demineralized water (H20), from 10 to 50 g/l of potassium hydroxide
or sodium hydroxide and from 20 to 100 g/l of ascorbic acid.
2. Method of production of a synthetic gas by electrolysis of a particular electrolyte,
as claimed in claim 1, where the electrolyte used in the apparatus or electrolyte
plant is composed of: for each 1000ml of demineralized water (H2O) from 10 to 50 grams
per liter of potassium hydroxide or sodium hydroxide and-from 20 to 50 grams per liter of Ascorbic Acid (C6H8O6).
3. Method of production of a synthetic gas by electrolysis of a particular electrolyte,
as claimed in claim 1 and 2, in which the electrolytic reaction, transforms the basic
solution in a flammable gas, usable directly and immediately.
4. Method of production of a synthetic gas by electrolysis of a particular electrolyte
as claimed in claim 1, 2 or 3, in which the operating temperature remains between
60 ° and 70 ° centigrade.
5. Method of production of a synthetic gas by electrolysis of a particular electrolyte,
as claimed in claims 1, 2, 3 or 4, wherein siad synthetic gas has the composition:
• From 53 % to 73% of Hydrogen (H)
• From 20 % to 32% of carbon dioxide (CO2)
• From 1 % to 3% of carbon monoxide (CO)
• From 1,5 % to 4% of oxygen (O)
• And some tens of parts per million by volume of hydrocarbons such as methane, ethane
+ ethylene, propane + propylene, butane + isobutane, pentane, hexane, methyl alcohol,
ethyl alcohol, isopropyl alcohol, benzene, toluene, ethylbenzene + chlorobenzene and
acetone.
1. Verfahren zur Herstellung eines synthetischen Gases durch Elektrolyse eines bestimmten
Elektrolyten, der aus Folgendem besteht: einer Lösung von entmineralisiertem Wasser
(H2O), Kaliumhydroxid (KOH) oder Natriumhydroxid (NaOH) und Ascorbinsäure (C6H8O6), wobei die Lösung für alle 1000 ml von entmineralisiertem Wasser (H2O) aus 10 bis 50 g/l Kaliumhydroxid oder Natriumhydroxid und aus 20 bis 100 g/l Ascorbinsäure
besteht.
2. Verfahren zur Herstellung eines synthetischen Gases durch Elektrolyse eines bestimmten
Elektrolyten gemäß Anspruch 1, worin der Elektrolyt, der in der Vorrichtung oder der
Elektrolytenanlage verwendet wird, aus Folgendem besteht: für alle 1000 ml von entmineralisiertem
Wasser (H2O), 10 bis 50 Gramm pro Liter Kaliumhydroxid oder Natriumhydroxid und 20 bis 50 Gramm
pro Liter Ascorbinsäure (C6H8O6).
3. Verfahren zur Herstellung eines synthetischen Gases durch Elektrolyse eines bestimmten
Elektrolyten gemäß Anspruch 1 und 2, worin die elektrolytische Reaktion die basische
Lösung in ein entflammbares Gas umwandelt, das sofort direkt nutzbar ist.
4. Verfahren zur Herstellung eines synthetischen Gases durch Elektrolyse eines bestimmten
Elektrolyten gemäß Anspruch 1, 2 oder 3, worin die Betriebstemperatur zwischen 60°
und 70° Celsius bleibt.
5. Verfahren zur Herstellung eines synthetischen Gases durch Elektrolyse eines bestimmten
Elektrolyten gemäß Anspruch 1, 2, 3 oder 4, worin das synthetische Gas folgende Zusammensetzung
hat:
• von 53% bis 73% Wasserstoff (H),
• von 20% bis 32% Kohlendioxid (CO2),
• von 1% bis 3% Kohlenmonoxid (CO)
• von 1,5% bis 4% Sauerstoff (O)
• und einige Zehnfache von Teilen je Million Teile nach Volumen von Kohlenwasserstoffen,
wie Methan, Ethan + Ethylen, Propan + Propylen, Butan + Isobutan, Pentan, Hexan, Methylalkohol,
Ethylalkohol, Isopropylalkohol, Benzen, Toluen, Ethylbenzen + Chlorbenzen und Aceton.
1. Procédé de production d'un gaz de synthèse par électrolyse d'un électrolyte particulier
se composant d'une solution d'eau déminéralisée (H2O), d'hydroxyde de potassium (KOH) ou d'hydroxyde de sodium (NaOH), et d'acide ascorbique
(C6H8O6), ladite solution se composant de, pour chaque 1000ml d'eau déminéralisée (H2O), de 10 à 50 g/l d'hydroxyde de potassium ou d'hydroxyde de sodium et de 20 à 100
g/l d'acide ascorbique.
2. Procédé de production d'un gaz de synthèse par électrolyse d'un électrolyte particulier
selon la revendication 1, dans lequel l'électrolyte utilisé dans l'appareil ou l'installation
électrolytique se compose de: pour chaque 1000 ml d'eau déminéralisée (H2O), de 10 à 50 grammes par litre d'hydroxyde de potassium ou d'hydroxyde de sodium
et de 20 à 50 grammes par litre d'acide ascorbique (C6H8O6).
3. Procédé de production d'un gaz de synthèse par électrolyse d'un électrolyte particulier
selon la revendication 1 ou 2, dans lequel la réaction électrolytique, transforme
la solution basique en un gaz inflammable, utilisable directement et immédiatement.
4. Procédé de production d'un gaz de synthèse par électrolyse d'un électrolyte particulier
selon la revendication 1, 2 ou 3, dans lequel la température de fonctionnement reste
entre 60° et 70° C.
5. Procédé de production d'un gaz de synthèse par électrolyse d'un électrolyte particulier
selon la revendication 1, 2, 3 ou 4, dans lequel ledit gaz de synthèse a la composition:
• de 53% à 73% d'hydrogène (H)
• de 20% à 32% de dioxyde de carbone (CO2)
• de 1% à 3% de monoxyde de carbone (CO)
• de 1,5% à 4% d'oxygène (O)
• et un peu (des dizaines de parties par million par volume) d'hydrocarbures tels
que le méthane, l'éthane + l'éthylène, le propane + le propylène, le butane + l'isobutane,
le pentane, l'hexane, le méthanol, l'éthanol, l'isopropanol, le benzène, le toluène,
l'éthylbenzène + le chlorobenzène et l'acétone.

REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only.
It does not form part of the European patent document. Even though great care has
been taken in compiling the references, errors or omissions cannot be excluded and
the EPO disclaims all liability in this regard.
Patent documents cited in the description